Integrated Robust and Resilient Control of Nuclear Power Plants for Operational Safety and High Performance,

IEEE TRANSACTIONS ON NUCLEAR SCIENCE, VOL. 57, NO. 2, APRIL 2010
807
Integrated Robust and Resilient Control of Nuclear
Power Plants for Operational Safety and
High Performance
Xin Jin, Student Member, IEEE, Asok Ray, Fellow, IEEE, and Robert M. Edwards
Abstract—This paper presents an integrated robust and resilient
control strategy to enhance the operational safety and performance
of nuclear power plants. The objective of robust control is to minimize the sensitivity of plant operations to exogenous disturbances
and internal faults while achieving a guaranteed level of performance with a priori specified bounds of uncertainties. On the other
hand, the role of resilient control is to enhance plant recovery from
unanticipated adverse conditions and faults as well as from emergency situations by altering its operational envelope in real time. In
this paper, the issues of real-time resilient control of nuclear power
plants are addressed for fast response during emergency operations while the features of the existing robust control technology
are retained during normal operations under both steady-state and
transient conditions. The proposed control methodology has been
validated on the International Reactor Innovative & Secure (IRIS)
simulator of nuclear power plants.
Low pass filter.
Index Terms—Emergency operation, nuclear power plant, operational safety, resilient control, robust control.
Augmented plant.
Field of complex and real numbers.
Disturbances and uncertainties.
Tracking error.
Lower LFT of plant P and controller K.
Strictly proper transfer function.
Robust controller.
Minimum-phase stable transfer function
matrix.
Nominal plant.
Solution of algebraic Lyapunov equation.
Reference Signals.
ACRONYMS
Temperatures of the nuclear power plant.
BIBO
Bounded-input bounded-output.
FSM
Finite state machine.
IRIS
International reactor innovative & secure.
LFT
Linear fractional transformation.
LOFA
Loss-of-flow accident.
MIMO
Multi-input multi-output.
RCP
Reactor coolant pump.
SISO
Single-input single-output.
Sampling time.
Controller outputs.
Outputs of robust and resilient controllers.
Disturbances.
Sensor noise.
Uncertainty input of
.
Control action weighting function.
Sensor noise weighting function.
Tracking error weighting function.
NOMENCLATURE
The variables that are used in the controller design procedure,
described in Sections II and IV-B, are listed below.
Uncertainty in plant modeling.
Measurement of plant output and its estimate.
Output estimation error
Manuscript received November 12, 2009; revised January 24, 2010. Current version published April 14, 2010. This work was supported in part by the
U.S. Department of Energy under NERI-C Grant DE-FG07-07ID14895 and by
NASA under Cooperative Agreement NNX07AK49A. Any opinions, findings
and conclusions or recommendations expressed in this publication are those of
the authors and do not necessarily reflect the views of the sponsoring agencies.
The authors are with the Department of Mechanical and Nuclear Engineering,
The Pennsylvania State University, University Park, PA, 16802 USA (e-mail:
[email protected]; [email protected]; [email protected]).
Color versions of one or more of the figures in this paper are available online
at http://ieeexplore.ieee.org.
Digital Object Identifier 10.1109/TNS.2010.2042071
Desired plant output following a desired
model.
Weighted control action.
Weighted tracking error.
Uncertainty output of
.
-norm of a transfer matrix operator.
0018-9499/$26.00 © 2010 IEEE
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IEEE TRANSACTIONS ON NUCLEAR SCIENCE, VOL. 57, NO. 2, APRIL 2010
State transition function of the FSM.
Set of all possible uncertainty
.
Block structure of plant uncertainties.
Block structure of performance objectives.
Structured singular value.
Vector of adaptive parameters and its
estimate.
Time constants.
I. INTRODUCTION
N
UCLEAR power plants are complex dynamical systems
with many variables that require dynamical adjustments
to achieve safety and efficiency over the entire operational envelope because their stability and performance could be severely
limited by a wide variety of safety requirements, operating conditions, internal faults, and exogenous disturbances. To achieve
the specified goals, multiple control variables are simultaneously manipulated for generating the required power and enabling the plant to exploit alternate decision and control strategies. These strategies are often dictated by economy and safety
of plant operations. For example, feedback regulation of nonlinear dynamics (e.g., control of reactor power and thermal hydraulics in the balance of plant) could lead to static bifurcation,
which is linked to degeneracy in the system’s zero dynamics [1].
When faced with unanticipated situations, such as equipment
failures or large exogenous disturbances to the plant control
system, the human operators are required to carry out diagnostic and corrective actions. Even experienced operators could
be overwhelmed by the sheer number of display devices and
sensor outputs to be monitored. An intelligent decision and control system with a large degree of autonomy could enhance the
operational safety and performance of nuclear plants by alleviating the burden of human operators and simultaneously mitigating the adverse consequences at an incipient stage.
Several researchers have reported intelligent decision and
control methods (e.g., optimal control [2], fuzzy logic [3],
neural networks [4], and model predictive control [5]) to enhance operational safety and performance of nuclear power
plants. Along this line, robust control techniques have also been
investigated [6], [7], where the role of a robust controller is
to achieve disturbance rejection by reducing sensitivity of the
plant control system (i.e., plant plus controller) to exogenous
disturbances and internal faults. The task is to synthesize a
robust decision and control law on an infinite-time horizon by:
• Mitigation of the detrimental effects of uncertainties and
exogenous disturbances;
• Trade-offs between plant stability and performance within
specified bounds of uncertainties [8].
However, stability and performance robustness of such control algorithms may not be assured beyond the a priori specified bounds of uncertainties and disturbances; usually larger are
the bounds, lower is the plant performance and plant instability
is less likely. Therefore, the bounds of structured and unstructured uncertainties are usually specified design parameters for
trade-off between stability and performance, and are often based
on nominal and off-nominal plant operations that may include at
most a few anticipated abnormalities. In the event of a plant accident, the deviations from the nominal plant operating conditions
may significantly exceed these uncertainty bounds. Hence, immediate actions beyond the regime of robust control are needed
for operational safety and subsequent restoration of normalcy to
the original operational mode or to a gracefully degraded mode.
Guo et al. [9] have investigated resilient propulsion control
of aircraft to determine on how engine control systems can improve safe-landing probabilities under adverse conditions. The
key idea is as follows: In emergency situations, the conservative procedure of engine control may not be suitable for aircraft
safety; it may be advantageous to compromise the engine health
to save the aircraft. The aim of their research is to develop adaptive engine control methodologies to operate the engine beyond
the normal domain for emergency operations to enhance safe
landing at the expense of possibly partial damage in the aircraft.
Motivated by this idea, resilient controllers can be designed for
nuclear power plants to ensure the operational safety by “sacrificing” performance under adverse conditions. Recently, Hovakimyan and coworkers [10] have reported a control algorithm
called -adaptive control to address the issues in Integrated Resilient Aircraft Control (IRAC) that is an active area of research
in National Aeronautics and Space Administration (NASA). It
is noted that the notion of resilience, introduced in the present
context, is entirely different from being non-fragile or insensitive to some errors in the nominal state-space matrices of controller during implementation [11].
The role of the proposed resilient control in a nuclear power
plant is to enhance recovery of the control system from unanticipated adverse conditions and faults as well as from emergency situations by altering its operational envelope in real time
[12]. Resilient decision and control laws are synthesized on a
finite-time horizon as augmentation of robust decision and control with the objectives of:
• Reliable and fast recovery from adverse conditions and
emergency situations;
• Restoration of the control configuration upon returning to
normalcy or upon graceful degradation within design specifications.
This paper addresses the issues of real-time resilient control of nuclear power plants for fast response during emergency
operations while the features of the existing robust controller
are retained during normal operating conditions. The goal is to
formulate and validate resilient and reconfigurable control algorithms toward deployment of real-time controllers for emergency recovery of nuclear plants from expected and unexpected
adverse conditions.
The integrated robust and resilient control strategy, developed
in this paper, has been tested on the International Reactor Innovative & Secure (IRIS) simulator [13], [14] that is built upon
one of the next generation nuclear reactor designs for a modular pressurized water reactor with an integral configuration.
Currently, IRIS is in the stage of pre-application licensing with
Nuclear Regulatory Commission (NRC); its safety testing for
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JIN et al.: INTEGRATED ROBUST AND RESILIENT CONTROL OF NUCLEAR POWER PLANTS
Design Certification (DC) is expected to be completed by 2010
with deployment in the 2015–2017 time frame.
The major contributions of the paper are delineated below:
• Introduction of the innovative concept of resilient control
in nuclear plant control for fast recovery from unanticipated adverse conditions and emergency situations.
• Extension of the concept of robustness by integration with
resilience for control of nuclear power plants under both
normal operations and emergency situations.
• Validation of the concept of integrated robust and resilient
control of nuclear power plants on the IRIS simulator.
The paper is organized in five sections including the present
one. Section II presents underlying principles of robust control and resilient control. Section III addresses integration of robust control and resilient control strategies. Section IV presents
testing and validation of these strategies on the IRIS simulator.
The paper is summarized and concluded in Section V.
II. ROBUST AND RESILIENT CONTROL
This section introduces the underlying principles of multivariable robust control and resilient control for nuclear power
-based
plants, where robust controllers are designed by the
-synthesis method [8] and resilient controllers are designed
by -adaptive output feedback algorithm [10]. A finite state
machine is then used to integrate the above two controllers for
normal operation and emergency recovery from both expected
and unexpected adverse conditions while bumpless transfer
between the control modes is assured by usage of smoothing
filters.
A. Robust Multivariable Control Using -Synthesis
In this paper, a -synthesis robust control approach is used to
synthesize the feedback controller. The plant uncertainties, including the effects of unmodeled dynamics, linearization, and
model reduction, are characterized and estimated. Based on the
specified uncertainties, robust multivariable controllers are designed using D-K iteration [8] based on the stability and performance specifications. The order of the synthesized controllers
is then reduced to an acceptable level by Hankel norm approximation [15].
1) Uncertainty Modeling: Uncertainties due to the inability
to model relevant dynamics in an actual plant and the simplification to achieve a mathematical representation, including linearization and model reduction, are taken into consideration for
synthesis of robust controllers. Consequently, robustness of the
synthesized controller is dependent on the type and size of the
uncertainties.
In the controller design for nuclear power plants, Shyu and
Edwards [7] considered three types of uncertainties due to unmodeled dynamics, linearization, and model reduction, respectively. These uncertainties contribute to the deviation between
the real plant and its reduced-order linear model, based on which
the robust controller is synthesized. The unmodeled uncertainties are obtained from the modeling process where the governing
equations are derived to represent the plant dynamics including
the errors induced by linearization and model reduction.
Unstructured uncertainties, represented by the difference of
the magnitude of input-output frequency response at each fre-
809
Fig. 1. Closed-loop system interconnection diagram.
quency point, are used in this paper. This bound is defined by the
norm of the uncertainty matrix. The overall uncertainty bound
is chosen to cover the summation of all uncertainties considered
above, i.e.,
(1)
where
is bound of the overall uncertainty,
is the
overall uncertainty which is the summation of the magnitudes
, model reduction uncertainty
of linearization uncertainty
, and unmodeled uncertainty
.
The uncertainty bounds are defined as in (2) in a diagonal
matrix form to cover the overall uncertainty. For the purpose of
robust controller design, it is advantageous to normalize uncer:
tainty with a frequency dependent weighting function
(2)
where
, and
.
2) Performance Specifications: Selection of weighting functions and interconnection of the closed-loop system is an essential step in the synthesis of a robust controller. The weighting
functions that specify the plant uncertainty and performance
specifications invariably need to be adjusted iteratively. Fig. 1
shows the block diagram of closed-loop control system with performance specifications, as explained below.
represents the in• The uncertainty weighting function
tegrated uncertainty bound.
specifies the per• The tracking error weighting function
formance requirements, which is chosen in such a way that
the steady-state tracking errors in both channels should be
small (e.g., on the order of 0.01 or less).
is used to atten• The control action weighting function
uate the control action efforts. That is, if the control action
is tuned offline to penalize the control efis excessive,
forts, and conversely if the plant response is sluggish.
represents the fre• The sensor noise weighting function
quency-dependent effects to filter the measurement noise.
Upon selection of the above weighting functions, the nomcan be interconnected with the weighting
inal plant model
,
,
, and
) to generate the augfunctions (i.e.,
, as shown in Fig. 1, where the input and
mented plant
output of
are:
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IEEE TRANSACTIONS ON NUCLEAR SCIENCE, VOL. 57, NO. 2, APRIL 2010
Fig. 3. Closed-loop system with the L -adaptive controller.
Fig. 2. LFT description of the robust control problem.
is the control input from controller, is the measurement of
plant output, and is the tracking error.
The robust control problem is formulated in a two-port framework using linear fractional transform (LFT) [8], as shown in
and
denote the numbers of outputs and inputs
Fig. 2. Let
of the uncertainty weighting function, respectively, and
and
denote the numbers of output and input of the performance
specification weighting functions, respectively. Then, the block
structure of the uncertainty model is defined as:
(3)
The first block of the uncertainty matrix corresponds to the
, used in modeling the plant uncertainty.
uncertainty block
includes the performance objectives in
The second block
the framework of the -synthesis [8]. The inputs to the second
block are the weighted control action and weighted tracking
error , and the outputs are the reference , disturbance
and sensor noise signals
.
3) Controller Design Using -Synthesis: To meet the control
objectives, a stabilizing controller is synthesized such that, at
, the structured singular value satiseach frequency
fies the following condition:
(4)
where
represents the linear fractional transformation
(LFT) [8] of and . The fulfillment of this condition guarantees robust performance of the closed-loop control system. The
-synthesis can be accomplished by using the D-K iteration tool
in MATLAB [15]. For faster computation, the controller order
could be reduced by eliminating the insignificant states by balanced realization and Hankel norm approximation [8], [15].
-adaptive controller are: (i) guaranteed fast adaptation,
of
and (ii) simultaneous tracking of the input and output signals
-controller is both
that are uniformly bounded. Since the
robust and adaptive, it is suitable for resilient control.
-Adaptive Output Feedback Control: The -adaptive
1)
control architecture was first presented by Cao and Hovakimyan
[10] using a state feedback approach in systems with constant
-adaptive control has been
unknown parameters. Later, the
extended to nonlinear time-varying systems in the presence of
multiplicative and additive unmodeled dynamics [16]. Its extension to output feedback control has been presented for a class of
uncertain systems [17] that allows for tracking arbitrary reference with guaranteed time-delay margin. In the work reported in
this paper, the -output feedback adaptive control architecture
has been employed to address the challenge of resilient control
of nuclear power plant, as shown in Fig. 3. While details on
the -adaptive controller are reported in recent literature [10],
[16], [17], the salient features are explained in terms of the following single-input single-output (SISO) system model.
(5)
where
is the control input,
is the system
is a strictly proper unknown transfer function of
output,
unknown relative degree
for which only a known lower
is available, and
is the time-debound
pendent disturbances and uncertainties. With a slight abuse of
,
, and
are respecnotation, Laplace transforms of
tively denoted as
,
, and
.
be a given bounded continuous reference input
Let
signal. The control objective is to design an adaptive output
such that the system output
feedback controller giving
tracks the reference input
following a desired model:
(6)
B. Resilient Control
The role of resilient control is to enhance recovery of the
control system from unanticipated adverse conditions and
faults as well as from emergency situations. Therefore, the
resilient controller should be re-configurable to accommodate
wide-range operations and faulty conditions, and this requires
the resilient controller to be both robust and adaptive. Recently,
Hovakimyan et al. [10] have developed a novel control al-adaptive control, to address the issues in
gorithm, called
Integrated Resilient Aircraft Control (IRAC). The advantages
is a minimum-phase stable transfer function of relwhere
ative degree
. The system equations in terms of the desired model are rewritten as:
(7)
where
is the disturbance.
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JIN et al.: INTEGRATED ROBUST AND RESILIENT CONTROL OF NUCLEAR POWER PLANTS
Closed-Loop Reference System: Let
and
be the reference control input and reference disturbance, respectively, of the closed-loop reference system that defines an
achievable control objective for the -adaptive controller such
that:
Given the vector
sional nullspace of
811
, let be the
, i.e.,
-dimen-
(15)
and let
(8)
(16)
where
is a low pass filter with DC gain
and
is a (possibly) time-varying function of
.
the reference output
and
are selected such that
The transfer matrices
at sampling instant (with
The update law for
the sampling time) as:
(17)
(9)
is stable and that the
bounded as:
-gain of the cascaded system is upper
being
where the state transition matrix
(18)
(10)
Then, the reference system in (8) is stable.
Referring to Fig. 3, individual components of the -adaptive
controller are described next.
,
State Predictor (Passive Identifier): Let (
,
) be the minimal realization of the stable transfer
. Hence,
is controllable and observmatrix
being Hurwitz. Then, the system in (5) is rewritten
able with
in the state-space setting as:
and
(19)
where
denotes a Cartesian basis vector in
with its first
element equal to 1 and other elements being 0.
Control Law: The control law is defined via the output of the
low-pass filter:
(20)
(11)
and the associated state predictor is given by:
(12)
The complete -adaptive controller consists of the state predictor in (12), the adaptation law in (17), and the control law
in (20), subject to the -gain upper bound in (10). The performance bounds of the -adaptive output feedback controller are
given by the following theorem:
Theorem 2.1 (Theorem 1 and Lemma 3 in [17]):
where
is the vector of adaptive parameters. Nomay not belong
tice that, in the state predictor equation
does belong to the space
to the space spanned by , while
spanned by
in (11).
Adaptation Law: Let be the solution of the following algebraic Lyapunov equation:
(21)
denotes the
norm (i.e., essential supremum
where
of the absolute value) of the function .
(13)
III. INTEGRATION OF ROBUST AND RESILIENT CONTROL
. From the properties of it follows that there
where
always exists a nonsingular
such that
(14)
This section describes how the robust controllers and resilient
controllers are integrated. A finite-state machine (FSM) [18] has
been adopted for discrete decision-making, which monitors the
conditions of the nuclear power plant via a fault detector and
controls the bumpless transfer between the robust and resilient
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Fig. 4. Layout of the integrated robust and resilient control system.
formance criteria; this is achieved by returning to state
state .
from
B. Bumpless Transfer
Fig. 5. Example of a finite state machine (FSM).
controllers. Fig. 4 depicts the layout of an integrated robust and
resilient control system that includes the robust controller, resilient controller, fault detector, finite state machine (FSM), a
set of reference points, and a filter bank for bumpless transfer.
The fault detector is extrinsic to both robust and resilient controllers.
A. Finite State Machine
A finite state machine (FSM) [18] is a 5-tuple
, where is a finite set called the states, is
a finite set called the alphabet,
is the state
is the start state, and
is the
transition function,
set of accepted states or final states.
Fig. 5 shows an example of a finite state machine (FSM)
that consists of two states
,
representing the normal operating condition and an anomalous
condition, respectively. The alphabet in this FSM is selected as
, where the symbol 0 represents the normal condition, and the symbol 1 represents the detection of anomaly (e.g.,
abrupt temperature change in primary coolant flow). A brief explanation of the FSM’s operation is presented below.
When the nuclear power plant is in the normal operating condition (i.e., the symbol of the alphabet is 0), the FSM is in state
. When an anomaly occurs in the plant, the symbol changes
from 0 to 1, and the FSM makes a transition to the anomalous
state . Accordingly, the control system takes necessary actions
(e.g., change of the feed water flow set point) are taken to keep
the nuclear power plant safe according to the above procedure.
The FSM stays in state until the plant is restored to the normal
condition when the symbol changes back to 0, and thus the FSM
makes the transition back to the normal state . The role of resilient control is to make the transition from state to state
as quickly and safely as possible to recover from unanticipated
adverse conditions/faults and emergency situations by altering
its operational envelope in real time. The control configuration
is restored upon returning to normalcy if the plant is not damaged, or to a gracefully degraded condition if the plant is partially damaged but still operable within specified safety and per-
Switching from one controller to another should entail as little
agitation (i.e., occurrence of undesirable transients) as possible.
By parallel operation of a non-active controller one could try to
drive its output signals towards the “correct” amplitude, so that
the resulting transients of the closed loop due to a transfer of
authority are as small as possible. This is known as the bumpless transfer problem for transition from one operating mode to
another.
Many bumpless transfer techniques have been developed
for application in scenarios with different constraints, such as
switching between manual and automatic control, filter and
controller tuning, scheduled and adaptive controller [19]. In
this paper, a piecewise linear filter is constructed to mitigate the
transients during switching between the robust controller and
the resilient controller. The key idea is explained below.
While the robust controller is active to perform in both steady
state and transient conditions under normal operation, the resilient controller becomes active to provide safety and recovery
to the plant during adverse conditions and emergency situations.
In order to achieve bumpless transfer from robust control to
resilient control and avoid abrupt changes in control actions,
piecewise linear filters are added to the controller outputs. The
is formulated as:
resulting control action
(22)
where
and
are outputs of the resilient controller and
and
are the filter
robust controller, respectively, and
transfer functions for the respective control actions.
C. Integrated Robust and Resilient Control Strategy
Following Fig. 4, the next task is to incorporate the finite
state machine (FSM) and filter banks within the plant control
system for bumpless transfer between the robust and resilient
controllers. For example, upon detection of a loss-of-flow accident (LOFA), as the primary coolant temperature crosses a specified threshold, this information activates the transition between
states of the FSM. The state transition function provides inputs to both blocks, namely, set points and filter banks, as seen
in Fig. 4. If a significant fault or emergency situation is detected
in the plant, the state transition in the FSM initiates a bump-
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JIN et al.: INTEGRATED ROBUST AND RESILIENT CONTROL OF NUCLEAR POWER PLANTS
813
less transfer between the two controllers and may also alter the
thresholds in the set points module. The altered thresholds are
then used as the new set points for the controller under the abnormal condition. Upon return to normalcy, robust control with
the original set points are resumed. In practice, a fault detection
system is needed to identify an abnormal incident as early as
possible, which necessitates incorporation of a fault detection
scheme within the integrated robust and resilient system. This
is a topic of future research.
IV. TESTING AND VALIDATION ON THE IRIS SIMULATOR
The proposed integrated robust and resilient control strategy
has been tested and validated on a simulator of nuclear plants.
The results of simulation are presented and further experimental
validation is planned on research reactors (e.g., Penn State’s
TRIGA research reactor [20]) in the future.
A. The International Reactor Innovative & Secure Simulator
The International Reactor Innovative & Secure (IRIS) simulator of nuclear power plants is based on the design of a
next-generation nuclear reactor. It is a modular pressurized
water reactor (PWR) with an integral configuration of all
primary system components. Fig. 6 shows the layout of the
primary side of the IRIS system that is offered in configurations
of single or multiple modules, each having a power rating of
1000 MWt (about 335 MWe) [14]. The nominal reactor core
inlet and outlet temperatures are 557.6 (292 ) and 626
(330 ), respectively. The pressurizer, eight steam generators,
and the control rod mechanism are integrated into the pressure
vessel with the reactor core. There is no huge pipe used to
connect these components. This design avoids the large loss of
coolant accident (LOCA). The whole control rod mechanism
is mounted inside the pressure vessel to avoid failures of the
control rod head penetration.
As shown in Fig. 6, the integral design of the primary side
also makes the containment vessel much smaller than the traditional pressure vessel of a PWR. The IRIS reactor coolant
pumps are of the spool type, and are located entirely within the
reactor vessel; only small penetrations for the electrical power
cables are required. The spool pump geometric configuration
provides high inertia/coastdown and high run-out flow capability that contributes to minimize or even mitigate the negative
consequences of loss-of-flow accidents (LOFAs).
A simulation testbed for testing and validation of control
algorithms has been developed under the project of Nuclear
Energy Research Initiative (NERI). The testbed is built using
MATLAB/SIMULINK. This SIMULINK model includes a reactor core model, a helical coil steam generator (HCSG) model.
The turbine is not explicitly modeled in the testbed since the
reactor’s operational safety is the major focus of this paper. The
simulation testbed is implemented on a Quad Core 2.83 GHz
CPU 8 GB RAM Workstation in the laboratory of Penn State.
Another two workstations with the same configuration are also
available for simulating a twin-unit plant operation scenario,
in which two workstations host an individual IRIS module,
and the third one hosts the controller to coordinate the plant
modules through a local network. This testbed is capable of
Fig. 6. Layout of the primary side of the IRIS system [14].
simulating normal operation conditions at different operational
modes as well as various faulty scenarios including:
• Actuator failures: Feedwater pump trip, malfunctions of
reactor coolant pump and control rod mechanism;
• Sensor failures: Malfunctions of temperature, pressure,
and flow-rate sensors;
• Internal faults: Uncertainties in fuel temperature coefficient of reactivity, coolant heat capacity, and feedwater
heat capacity.
B. Design of the Integrated Robust and Resilient Control
System
The details of the integrated control system design are introduced in this section.
1) Robust Controller Design: The design of a robust controller requires judicious selection of the uncertainty weighting
and the performance weighting functions,
,
function
and
. These weighting functions essentially serve as
user-selected performance specifications.
is selected to capThe uncertainty weighting function
ture the frequency-dependent uncertainties as:
(23)
In order that the plant output tracks the given reference
signal , the tracking error weighting functions with respect to
each plant output are chosen and put into a form of the diagonal
as:
matrix
(24)
This weighting function indicates that the steady-state (i.e., lowfrequency) tracking errors due to reference step-inputs in either
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IEEE TRANSACTIONS ON NUCLEAR SCIENCE, VOL. 57, NO. 2, APRIL 2010
TABLE I
RESULTS OF THE -SYNTHESIS
TABLE II
ORDER REDUCTION OF CONTROLLER #5
channel should be on the order of 0.01 or smaller. This performance requirement becomes less stringent at high frequencies.
is included to
The control action weighting function
tune the control action effort. For example, if the time response
of the controlled system displays excessive control action,
the weighting function serves to penalize the energy of the
oscillation; on the other hand, if the response is sluggish, the
weighting function has a more benign role with a significantly
reduced penalty. The control action weighting function is
selected as:
[8], [15] has been used; the results of controller order reduction
are listed in Table II. It is seen in Table II that the -values
do not increase significantly after order-reduction until the
controller order is reduced below 10. There is a clear increase
in as the controller order is reduced from 7 to 6, and the value
of for controller order less than 6 is greater than 1. Therefore,
the controller of reduced order 7 is selected.
2) Resilient Controller Design: The resilient control algorithm in Section II-B is derived for a single-input single-output
(SISO) system. However, the plant dynamics of the IRIS model
are coupled in two sensor channels, steam pressure and reactor
power, which require an extension of the SISO
-adaptive
output feedback controller to multi-input multi-output (MIMO)
systems. The components of the MIMO control system are described below.
Desired System: The matrix transfer function of the desired
control system is selected in the following form:
(25)
In the closed-loop interconnection, effects of frequency-dependent sensor noise are represented by the weighting function
as:
diagonal matrix
(28)
(26)
An increased sensor noise weight makes the controller more
robust to sensor noise possibly at the expense of relatively slow
response.
The -synthesis design of the robust controller is accomplished by using the D-K iteration tool in MATLAB [15]. For
the IRIS plant, the results of D-K iterations are shown in Table I,
-norm of the transfer matrix operator that is
where is the
a measure of the controller’s robust stability, and is the structured singular value that is a measure of the controller’s robust
and
, the robust
performance. For controllers with
stability and robust performance are guaranteed. The controller
is selected after five D-K iterations as it yields the smallest
and values. The resulting robust controller of order with
(sensor) inputs and (control action) outputs in the state space
, is shown below:
form, where
where
and
are the scalar transfer functions for
corresponding channels of secondary steam pressure and reactor
power, where zero non-diagonal elements of the matrix transfer
function imply decoupling of the channels in the desired transfer
function. In the current design, minimum-phase stable transfer
are selected as:
functions of relative degree
(29)
where
,
. The parameter
and
are
chosen in such a way that the frequency response of the desired
system is close to that of the linearized IRIS model.
Low-Pass Filter: Following Fig. 4, the low-pass filter bank is
selected as:
(30)
(27)
As seen in Table I, the synthesized controller yields the
after five iterations and the robust perclosed-loop
formance of the control system is guaranteed for the prescribed
uncertainty and performance. For faster computation, the controller order is reduced by eliminating the insignificant states,
where balanced realization and Hankel norm approximation
(31)
where
,
. The structure and parameters of the
in
low-pass filter are chosen in such a way that system
(9) is stable and the -stability condition in (10) is satisfied.
Consequently, the closed-loop reference system in (8) is stable.
3) Smoothing Filter Design for Bumpless Transfer: Bumpless transfer between the robust and resilient controllers is
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JIN et al.: INTEGRATED ROBUST AND RESILIENT CONTROL OF NUCLEAR POWER PLANTS
Fig. 7. Normalized plant outputs.
achieved by incorporating smoothing filters. During the transition from a normal condition (i.e., state ) to an abnormal
condition (i.e., state ), the filter transfer functions are chosen
as:
(32)
and, during the transition from an abnormal condition (i.e., state
) to an normal condition (i.e., state ), the filter transfer functions are chosen as:
(33)
such that the control actions during transition stages are actually
a linear combination of time-dependent weighted outputs from
and
of the resilient and robust
the controller actions,
controllers and vice versa. The respective time constants and
are chosen according to performance specifications based on
the following rationale: While a large time constant yields slow
and smooth transition, a small time constant ensures fast response. In this study, the time constants and are chosen as 2
sec and 200 sec, respectively. The smaller value of represents
relatively rapid response that is needed for transition to resilient
control to deal with emergency situations. The larger value of
represents relatively slow response for transition back to robust
control as normalcy is restored.
A -analysis test confirms that bounded-input boundedoutput (BIBO) stability of the augmented closed-loop system
and
.
is retained after the addition of the filters,
Synthesis of a more advanced filter is a topic of future research.
C. Results of Testing and Validation on the IRIS Simulator
A scenario of loss-of-flow accident (LOFA) for the (closed
loop) system has been simulated on the IRIS to evaluate the
performance of integrated robust and resilient control algorithm. Example of causes for LOFA are loss of off-site power,
pump failure, heat exchanger blockage, pipe blockage, and
faulty valve closure. In this simulation, the LOFA is caused
by reactor coolant pump (RCP) failure of 4 out of 8 reactor
coolant pumps, which is a Condition IV accident. Although
this accidental event can be mitigated by the “Safe-by-Design”
feature of IRIS [14] (i.e., natural circulation of coolant removes
decay heat from the core even when the coolant pump fails),
the plant could still be damaged if appropriate control actions
are not taken.
In the first 100 sec of the simulation exercise, the nuclear
power plant is in a normal operating condition with full output
815
power load and steam pressure load. In the simulated scenario,
when four of the eight primary flow pumps fail, the LOFA is
and the resulting anomaly information
detected at
is generated as seen in Fig. 4. The fault detection system is extrinsic to both the robust and resilient controllers, and its incorporation within the integrated control system is a topic of future
research.
Upon detection of the LOFA incident, the control output
is switched quickly from the robust controller to the resilient
controller that promptly reduces the set points of output power
load and feedwater flow by half. The plant is brought back to
when all primary flow pumps become
normalcy at
functional. To make the plant return to normalcy, the output
power load and feedwater flow set points are reset to their
respective nominal values, and the control output is switched
bumplessly from the resilient controller back to the robust
controller. Note that this bumpless transfer is ensured by the
choice of a relatively large filter time constant
relative to the tenure of the LOFA.
Fig. 7 shows the normalized plant outputs, steam pressure
and reactor output power . Under normal conditions, both
plant outputs are at their nominal values, which are normalized
to 1. When four of the eight primary reactor coolant pumps
fail, the plant is not able to generate 100% power, and thus the
output power load is reduced to 50% by resilient control actions. Upon returning to normalcy, the output power gradually
returns to 100%. Note that there exist spikes in the reactor power
when the anomaly occurs and it is removed. Those spikes
are generated due to temperature feedback from the reactor as
a consequence of the abrupt change in primary flow when four
of the eight pumps fail. Note that, in practice, a change in the
feedwater flow may not occur as a step, but may have a relatively more gradual but sufficiently fast profile. Furthermore, if
the output power in the control system is taken to be the turbine
output power instead of the reactor core output power, the spikes
would be averaged out due to the mechanical inertia of the turbine. In the future work, a turbine model will be integrated into
the nuclear plant model.
Fig. 8 shows the responses of the control actions, feedwater
and rod reactivity , after occurrence of the LOFA.
flow
When the plant is operated under normal conditions, the control
efforts are indicated as 0% implying zero deviations from the
and . Upon detection of the LOFA at
nominal values of
, in order to “save” the plant, the feedwater flow is
gradually increased by 10% of the nominal value and the rod
reactivity is reduced by more than 80% of the nominal value.
Fig. 9 shows the temperatures (i.e., primary coolant inlet, primary coolant outlet, and secondary coolant steam temperatures)
is the temperamonitored by sensors inside the plant, and
ture difference between the primary coolant inlet flow and outlet
flow, which is used to activate the FSM (see Figs. 5 and 4). Upon
detection of the LOFA, the control system reduces the rod reactivity by more than 80%. Consequently, the primary coolant
inlet temperature drops.
As seen in Fig. 10, switching of the symbols (i.e., 0 and 1)
of the alphabet are controlled by the FSM. When the plant is
working in normal conditions, the symbol is 0, the FSM stays
in normal state , and the output power reference point is 1.
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IEEE TRANSACTIONS ON NUCLEAR SCIENCE, VOL. 57, NO. 2, APRIL 2010
Fig. 8. Control actions of integrated robust and resilient controller.
Fig. 9. Temperatures of steam, primary inlet and outlet flows.
A simple scenario of loss-of-flow accident (LOFA) has been
investigated on the International Reactor Innovative & Secure
(IRIS) simulator [14]. Simulation results based on this LOFA
scenario show that the proposed controller recovers from the
emergency situation with a fast response, while the characteristics of the standard robust controller are retained during normal
operating conditions. Further analytical, simulation and experimental research is necessary before this novel concept of integrated robust and resilient control can be considered for application to commercial nuclear power plants. The following are
a few examples of future research in integrated robust and resilient control of nuclear power plants:
• Incorporation of fault detection schemes within the integrated control system;
• Filter design for fast and stable switching between robust
and resilient control modes;
• Construction of finite-state machines for incorporation
within the integrated control system to represent various
failure states and interstate switching;
• Demonstration of safe recovery from various real-life
emergency situations by including balance of plant components in the IRIS simulator;
• Experimental validation of safe recovery under selected
accident scenarios on research reactors (e.g., Penn State’s
TRIGA research reactor [20]).
ACKNOWLEDGMENT
Fig. 10. Finite state machine alphabets and output power set point changes.
When the anomaly occurs, the symbol changes to 1 immedito
and
ately, which causes the FSM to transit from state
the output power reference point to change from 1 to 0.5.
V. SUMMARY, CONCLUSIONS & FUTURE WORK
This paper investigates a new concept of integrated robust and
resilient control for enhancement of the operational safety and
performance of nuclear power plants. The robust controller is
designed by using the -synthesis tools with D-K iteration [15].
The optimal Hankel approximation is used to reduce the order
of the robust controller [15]. The concept of resilient control
in nuclear plants is derived from Integrated Resilient Aircraft
Control (IRAC) [9] that is an active area of research in National Aeronautics and Space Administration (NASA); this is
a direct transfer of technology from aeronautics to nuclear engineering. The resilient control is implemented by -adaptive
output feedback controller, which guarantees fast adaptation,
uniformly bounded transient and asymptotic tracking for both
input and output signals of the control system simultaneously.
The robust and resilient controllers are integrated by utilizing
a finite state machine and smoothing filters to ensure bumpless
transfer from robust to resilient control modes and vice versa.
In the simulation example of nuclear power plant control, the
finite state machine is designed to switch between normal and
abnormal states and activate related control actions by monitoring plant coolant temperatures. The filters ensure bumpless
transfer between robust controller and resilient controller and
avoid impact to the nuclear reactor during transition stage.
The authors would like to thank Prof. Naira Hovakimyan of
the University of Illinois at Urbana Champaign for her technical
support in developing the resilient controller. The authors are
also grateful to the thoughtful and meticulous comments of the
anonymous reviewers.
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